EP0176727B1 - Verfahren zur Herstellung von kugelförmigen Brennelementen - Google Patents
Verfahren zur Herstellung von kugelförmigen Brennelementen Download PDFInfo
- Publication number
- EP0176727B1 EP0176727B1 EP85110317A EP85110317A EP0176727B1 EP 0176727 B1 EP0176727 B1 EP 0176727B1 EP 85110317 A EP85110317 A EP 85110317A EP 85110317 A EP85110317 A EP 85110317A EP 0176727 B1 EP0176727 B1 EP 0176727B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- furnace
- binder resin
- sphere
- temperature
- resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000446 fuel Substances 0.000 title claims description 8
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000011230 binding agent Substances 0.000 claims description 28
- 229920005989 resin Polymers 0.000 claims description 27
- 239000011347 resin Substances 0.000 claims description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 11
- 238000004939 coking Methods 0.000 claims description 11
- 239000006096 absorbing agent Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 claims description 8
- 239000011159 matrix material Substances 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- 239000000843 powder Substances 0.000 claims description 8
- 229910002804 graphite Inorganic materials 0.000 claims description 7
- 239000010439 graphite Substances 0.000 claims description 7
- 238000010926 purge Methods 0.000 claims description 7
- 229920003002 synthetic resin Polymers 0.000 claims description 6
- 239000000057 synthetic resin Substances 0.000 claims description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 5
- 235000010299 hexamethylene tetramine Nutrition 0.000 claims description 4
- 239000004312 hexamethylene tetramine Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 239000003758 nuclear fuel Substances 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 239000000571 coke Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims description 2
- 238000001354 calcination Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 9
- 229920001187 thermosetting polymer Polymers 0.000 description 7
- 238000005336 cracking Methods 0.000 description 4
- 238000011010 flushing procedure Methods 0.000 description 3
- 229960004011 methenamine Drugs 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 229920001169 thermoplastic Polymers 0.000 description 3
- 239000004416 thermosoftening plastic Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000000137 annealing Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910021382 natural graphite Inorganic materials 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C21/00—Apparatus or processes specially adapted to the manufacture of reactors or parts thereof
- G21C21/02—Manufacture of fuel elements or breeder elements contained in non-active casings
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Definitions
- the invention relates to a method for producing spherical fuel or absorber elements for high-temperature reactors, consisting of a graphical matrix and coated particles embedded therein, by pressing a mixture of graphite press powder containing binder resin with coated nuclear fuel or absorber particles into a ball, coking the binder resin in one Furnace with gas flushing and vacuum annealing up to approx. 2000 ° C.
- Spherical fuel or absorber elements for high temperature reactors such as. B. described in DE-PS 1909871, contain the nuclear fuel or absorber in the form of coated particles, a graphitic matrix are embedded.
- this matrix material finely ground, highly crystalline types of natural and / or electrographite are mixed with a binder resin and further processed to a so-called graphite press powder by means of mixing or kneading processes and renewed grinding to desired grain size.
- the coated particles are mixed with graphite powder and, if necessary, after an additional coating step in which they are coated with a 100 [.lm thick layer of pressed powder, in order to form spherical fuel elements.
- the binder resin is then coked to carbon in a coking step, followed by cleaning and degassing of the elements, which are annealed in a vacuum at temperatures above 1600 ° C.
- pitches and thermoplastic and thermosetting synthetic resins are possible, in particular thermoplastic and thermosetting synthetic resins based on phenol are used.
- binder resins When these binder resins are coked, organic cracking products are produced. Furthermore, especially when thermoplastic synthetic resins or pitches are used, the binder temporarily softens during the temperature rise at the beginning of the coking process. During this phase, the dimensional stability of the fuel or absorber element compacts is reduced.
- the compacts must be stored in such a way that their own weight means that there is no inadmissible deformation during the softening phase of the binder resin, or thermosetting binder resins must be used to maintain the shape stability.
- the compacts can also be coked in a pusher furnace. The balls must be transported individually in a suitable boat through the furnace to prevent possible mutual contact and sticking or an inadmissible deformation. In all cases, the cracked products are removed from the coking ovens by so-called purge gases.
- thermosetting synthetic resin is used as the binder resin.
- This object was achieved according to the invention in that after the balls had been pressed, this binder resin was first fully cured at temperatures between 110 and 170 ° C. for at least 4 hours, and in that the balls were then coked within 2 to 10 hours to coke the binder resin pass through a furnace inclined downwards to 12 ° against the horizontal, the furnace having a temperature profile rising from the ball addition side to the ball removal side from around 100 to 800 to 1000 ° C and steeply falling from 800 to 1000 ° C to around 100 ° C, and in that Purge gas is fed from the furnace both from the ball addition side and from the ball removal side and is discharged in the furnace area at a temperature of 400 to 500 ° C on the increasing temperature profile branch.
- a synthetic resin based on phenol and hexamethylenetetramine is preferably used as the binder resin.
- the furnace temperature should not exceed a maximum value of 800 to 1000 ° C, whereby this temperature must be maintained over 10 to 20% of the furnace length. It has also proven to be advantageous if the furnace inclination is 3 to 10 ° with respect to the horizontal.
- thermosetting binder resins preferably based on phenol / hexamethylenetetramine, are used and coking is preceded by a separate process step in which this binder resin, after shaping the fuel or absorber elements, initially at temperatures between
- thermosetting binder resin of the matrix material had completely hardened
- the special guidance of the purge gas in the coking oven also removed the non-volatile cracking products so reliably that balls stuck together or a deposit of cracked product residues in the flow channel , which would hinder the free rolling, is prevented.
- the combined use of a hardened thermosetting binder resin with the purge gas guide described makes it possible to continuously roll balls as an uninterrupted column through the oven, the balls being able to touch each other without any problems, and to achieve high throughputs. The use of transport aids is not necessary.
- a thousand spheres are produced using a graphite press powder which consists of 78% finely ground natural graphite / electrographite powder mixture and 22% binder resin (phenol and hexamethylene tetramine in a ratio of 5: 1 - 10: 1). After pressing, the compacts were exposed to a temperature of 150 ° C for about 4 hours, during which the binder was fully cured.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Plasma & Fusion (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Carbon And Carbon Compounds (AREA)
- Ceramic Products (AREA)
- Fuel Cell (AREA)
- Catalysts (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843435861 DE3435861A1 (de) | 1984-09-29 | 1984-09-29 | Verfahren zur herstellung von kugelfoermigen brennelementen |
DE3435861 | 1984-09-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0176727A1 EP0176727A1 (de) | 1986-04-09 |
EP0176727B1 true EP0176727B1 (de) | 1988-07-13 |
Family
ID=6246729
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP85110317A Expired EP0176727B1 (de) | 1984-09-29 | 1985-08-17 | Verfahren zur Herstellung von kugelförmigen Brennelementen |
Country Status (4)
Country | Link |
---|---|
US (1) | US4666639A (enrdf_load_stackoverflow) |
EP (1) | EP0176727B1 (enrdf_load_stackoverflow) |
JP (1) | JPS6190088A (enrdf_load_stackoverflow) |
DE (2) | DE3435861A1 (enrdf_load_stackoverflow) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8900069B2 (en) | 2010-12-28 | 2014-12-02 | Taylor Made Golf Company, Inc. | Fairway wood center of gravity projection |
US20060176995A1 (en) * | 2005-02-10 | 2006-08-10 | Arizona Public Service Company | Control arrangement for use with nuclear fuel |
US9707457B2 (en) | 2010-12-28 | 2017-07-18 | Taylor Made Golf Company, Inc. | Golf club |
US8888607B2 (en) | 2010-12-28 | 2014-11-18 | Taylor Made Golf Company, Inc. | Fairway wood center of gravity projection |
US10639524B2 (en) | 2010-12-28 | 2020-05-05 | Taylor Made Golf Company, Inc. | Golf club head |
US10653926B2 (en) | 2018-07-23 | 2020-05-19 | Taylor Made Golf Company, Inc. | Golf club heads |
US11759685B2 (en) | 2020-12-28 | 2023-09-19 | Taylor Made Golf Company, Inc. | Golf club heads |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1158641B (de) * | 1960-02-24 | 1963-12-05 | Degussa | Verfahren zur Herstellung von Brennelementen fuer Kernreaktoren |
DE1286228B (de) * | 1964-08-07 | 1969-01-02 | Union Carbide Corp | Verfahren zur Herstellung eines Kernbrennstoffelementes |
AT270831B (de) * | 1964-08-07 | 1969-05-12 | Union Carbide Corp | Brennstoffelement für Kernreaktoren |
FR1520232A (fr) * | 1966-04-28 | 1968-04-05 | Euratom | élément de combustible nucléaire et procédé pour sa préparation |
AT276583B (de) * | 1967-12-07 | 1969-11-25 | Oesterr Studien Atomenergie | Höchsttemperaturbeständige Teilchen für die Kernenergieerzeugung sowie Verfahren zu deren Herstellung |
GB1256033A (en) * | 1969-08-06 | 1971-12-08 | Atomic Energy Authority Uk | Improvements in or relating to nuclear fuel |
GB1301880A (enrdf_load_stackoverflow) * | 1970-12-29 | 1973-01-04 | ||
DE2348282C3 (de) * | 1973-09-26 | 1979-02-01 | Hobeg Hochtemperaturreaktor-Brennelement Gmbh, 6450 Hanau | Verfahren zur Herstellung von Graphitpreßpulver und Graphitpreßmassen zur Fertigung von Graphitformkörpern |
JPS5324596B2 (enrdf_load_stackoverflow) * | 1974-03-22 | 1978-07-21 | ||
US4035452A (en) * | 1975-01-21 | 1977-07-12 | General Atomic Company | Method of making nuclear fuel bodies |
US4073834A (en) * | 1975-03-05 | 1978-02-14 | General Atomic Company | Method of making nuclear fuel elements |
US4140738A (en) * | 1976-03-08 | 1979-02-20 | Hobeg Hochtemperaturreaktor-Brennelement Gmbh | Process for the production of block fuel elements for high temperature reactors |
JPS58191998A (ja) * | 1982-05-06 | 1983-11-09 | 動力炉・核燃料開発事業団 | 環状槽型マイクロ波加熱装置 |
-
1984
- 1984-09-29 DE DE19843435861 patent/DE3435861A1/de active Granted
-
1985
- 1985-08-17 EP EP85110317A patent/EP0176727B1/de not_active Expired
- 1985-08-17 DE DE8585110317T patent/DE3563799D1/de not_active Expired
- 1985-09-04 US US06/772,394 patent/US4666639A/en not_active Expired - Lifetime
- 1985-09-27 JP JP60212782A patent/JPS6190088A/ja active Granted
Also Published As
Publication number | Publication date |
---|---|
DE3563799D1 (en) | 1988-08-18 |
JPS6190088A (ja) | 1986-05-08 |
US4666639A (en) | 1987-05-19 |
JPH0546918B2 (enrdf_load_stackoverflow) | 1993-07-15 |
DE3435861C2 (enrdf_load_stackoverflow) | 1987-11-12 |
EP0176727A1 (de) | 1986-04-09 |
DE3435861A1 (de) | 1986-04-03 |
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